JPS6244742Y2 - - Google Patents

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Publication number
JPS6244742Y2
JPS6244742Y2 JP5129880U JP5129880U JPS6244742Y2 JP S6244742 Y2 JPS6244742 Y2 JP S6244742Y2 JP 5129880 U JP5129880 U JP 5129880U JP 5129880 U JP5129880 U JP 5129880U JP S6244742 Y2 JPS6244742 Y2 JP S6244742Y2
Authority
JP
Japan
Prior art keywords
pipe
coal
pulverized coal
slurry
powdered coal
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP5129880U
Other languages
Japanese (ja)
Other versions
JPS56151350U (en
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed filed Critical
Priority to JP5129880U priority Critical patent/JPS6244742Y2/ja
Priority to US06/247,188 priority patent/US4401278A/en
Priority to GB8109521A priority patent/GB2073649B/en
Priority to DE3111854A priority patent/DE3111854C2/en
Priority to CA000374078A priority patent/CA1162045A/en
Publication of JPS56151350U publication Critical patent/JPS56151350U/ja
Application granted granted Critical
Publication of JPS6244742Y2 publication Critical patent/JPS6244742Y2/ja
Expired legal-status Critical Current

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  • Glanulating (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Description

【考案の詳細な説明】 本考案は粉炭の造粒装置に関する。[Detailed explanation of the idea] The present invention relates to a pulverized coal granulation device.

一般に、石炭をスラリー輸送により貯蔵庫まで
輸送する場合、このスラリー輸送に供される石炭
は輸送動力やその破砕の点から、比較的粒度範囲
の広い粉炭である。このような粉炭は輸送には都
合は良いが、貯蔵庫内で沈下する時に偏析し、そ
の結果、粉炭を脱水する場合に脱水効率が低下し
たり又は粉炭を貯蔵庫から取り出す時にブリツジ
現象を起こすなどの問題があつた。これらの問題
を解決する方法として、スラリー状の粉炭を造粒
すれば良いことが分かつている。しかし粉炭の粒
度範囲は広く、既存のラインミキサーなどの造粒
装置では粒度範囲の広い粉炭に結合剤を分散させ
ながら造粒することは困難である。
Generally, when coal is transported to storage by slurry transport, the coal used for slurry transport is pulverized coal with a relatively wide particle size range in terms of transportation power and crushing. Although this type of pulverized coal is convenient for transportation, it segregates when it sinks in storage, resulting in a decrease in dehydration efficiency when dehydrating pulverized coal, or a bridging phenomenon when taking pulverized coal out of storage. There was a problem. It has been found that a method for solving these problems is to granulate slurry-like powdered coal. However, the particle size range of powdered coal is wide, and it is difficult to granulate powdered coal with a wide particle size range while dispersing a binder using existing granulation equipment such as line mixers.

そこで、本考案は以上の問題を解決するために
成されたもので、その目的はスラリー状粉炭を効
率良く造粒する装置を提供することにある。
Therefore, the present invention was made to solve the above problems, and its purpose is to provide an apparatus for efficiently granulating slurry powdered coal.

以下、本考案の一実施例を第1図及び第2図に
基づき説明すると、1はスラリー状粉炭の輸送流
路を形成する管である。2は軸体で、上記管1の
小区間の直線部1a内に且つ管1の軸心に一致し
て設けられた軸体で、その一端は直線部1aの一
端コーナ外側部1bに回転可能に且つ液密に支持
され、また他端は直線部1aの他端コーナ外側部
1cを回転可能に且つ液密に貫通すると共に駆動
装置(図示せず)に接続されている。3は金網状
の撹拌翼で、上記軸体2の複数箇所に設けられて
いる。また、上記撹拌翼3の外周端と管1の内面
との間には隙間aを有するようにされている。
Hereinafter, one embodiment of the present invention will be described based on FIGS. 1 and 2. Reference numeral 1 indicates a pipe forming a passage for transporting slurry powdered coal. Reference numeral 2 denotes a shaft body, which is provided within the straight section 1a of the small section of the tube 1 and aligned with the axis of the tube 1, and one end of which is rotatable to the outer side 1b of one end corner of the straight section 1a. The other end rotatably and liquid-tightly penetrates the other end corner outside portion 1c of the straight portion 1a, and is connected to a drive device (not shown). Reference numeral 3 designates wire-mesh-like stirring blades, which are provided at multiple locations on the shaft body 2 . Further, a gap a is provided between the outer peripheral end of the stirring blade 3 and the inner surface of the tube 1.

以上のような構成によると、管1内を流れてき
たスラリー状の粉炭と結合剤(例えば灯油、軽
油、重油、残査油、植物油)は金網状の撹拌翼3
によつて混合撹拌される。そして、比較的大きな
粒子の粉炭に微細な粉炭が付着凝集して造粒され
ていく。この時、粉炭の移動状態は第2図の矢印
で示すようなものとなり、従来のような管路内に
羽根形の邪魔板を設けただけのスタテイクミキサ
ーや通常の羽根を有する撹拌機を設けたラインミ
キサーなどの装置と違つた動きを示している。即
ち、管1内での造粒炭及び粉炭粒子の動きあるい
は壁面での転動が造粒を進める上で効果的な作用
を行なつている。こうして、管1の直線部1aで
造粒された造粒炭は隙間aを通つて下流に流れて
いく。また、造粒の進行速度が早い造粒炭は撹拌
翼3,3間で早目に落下して他の粉炭の造粒作用
をスムースにさせる。
According to the above configuration, the slurry powdered coal and binder (for example, kerosene, light oil, heavy oil, residual oil, vegetable oil) flowing through the pipe 1 are passed through the wire mesh stirring blades 3.
The mixture is mixed and stirred by Then, fine powdered coal adheres to and aggregates with relatively large particles of powdered coal and is granulated. At this time, the state of movement of the pulverized coal is as shown by the arrow in Figure 2, and it is difficult to use a static mixer that simply has a vane-shaped baffle plate in the conduit or an agitator that has ordinary vanes. The movement is different from that of the installed line mixer and other equipment. That is, the movement of the granulated coal and powdered coal particles within the tube 1 or rolling on the wall has an effective effect on advancing granulation. In this way, the granulated coal granulated in the straight portion 1a of the pipe 1 flows downstream through the gap a. Further, the granulated coal whose granulation progresses quickly falls between the stirring blades 3 and 3 quickly, thereby smoothing the granulation action of other powdered coal.

次に、別の実施例を第3図及び第4図に基づい
て説明する。本実施例のものはスラリー状粉炭輪
送管途中の複数段に設けられた曲管部11内にそ
れぞれ撹拌翼12を設けたものである。即ち、曲
管部11を水平管11aと、該水平管11aから
斜め上方に延設されて且つその端部に盲部11c
を有する折曲管11bとから構成し、該折曲管1
1b内に複数個の撹拌翼12を有する軸体13を
盲部11cを回転可能に貫通して設け、該軸体1
3に駆動装置(図示せず)を接続したものであ
る。そして、この曲管部11は水平管11aの折
曲管11bとの接続近傍の接続部14に他の曲管
部11の水平管11aの端部が接続されて順次複
数段連続して設けられている。
Next, another embodiment will be described based on FIGS. 3 and 4. In this embodiment, stirring blades 12 are provided in each of the curved pipe portions 11 provided at multiple stages in the middle of the slurry powder coal ring feed pipe. That is, the bent pipe portion 11 is formed into a horizontal pipe 11a, which extends obliquely upward from the horizontal pipe 11a, and has a blind portion 11c at the end thereof.
The bent tube 11b has a bending tube 11b.
A shaft body 13 having a plurality of stirring blades 12 is provided in 1b so as to rotatably penetrate the blind portion 11c, and the shaft body 1
3 is connected to a drive device (not shown). The bent pipe section 11 is successively provided in multiple stages, with the end of the horizontal pipe 11a of the other bent pipe section 11 connected to the connecting part 14 near the connection of the horizontal pipe 11a with the bent pipe 11b. ing.

このような構成によると、スラリー状粉炭は曲
管部11内では矢印のような動きを示し、結合剤
と一層効率よく混合撹拌されて、広い粒度範囲の
粉炭を効率よく造粒することができる。
According to such a configuration, the slurry-like pulverized coal moves like an arrow within the curved pipe section 11, and is mixed and stirred with the binder more efficiently, making it possible to efficiently granulate pulverized coal with a wide particle size range. .

なお、撹拌翼は前記実施例で説明したようなも
のに限られるものではなく、例えば実施例で説明
したような円形状のものを軸体に対して斜めに取
り付けたものでも良く、また第5図に示すよう
に、前記実施例の各撹拌翼21の両側に且つ軸体
22に沿つて放射状に複数個の翼23を取り付け
たものでも良い。更に、第1図及び第3図を前記
各実施例の正面図として説明したが、平面図とし
て考えたものでも良い。
Incidentally, the stirring blade is not limited to the one explained in the above embodiment, but may be a circular one as explained in the embodiment, which is attached obliquely to the shaft body. As shown in the figure, a plurality of blades 23 may be attached radially on both sides of each stirring blade 21 of the above embodiment and along the shaft body 22. Furthermore, although FIGS. 1 and 3 have been described as front views of the respective embodiments, they may also be considered as plan views.

以上のように、本考案の粉炭の造粒装置によれ
ば、管路内に設けられた複数個の金網状の撹拌翼
によつて、スラリー状粉炭と結合剤を混合撹拌す
るようにしているので、粉炭を既存の装置とは違
つた動きをさせることができ、粒度範囲の広い粉
炭を効果的に造粒することができる。
As described above, according to the powdered coal granulation device of the present invention, the slurry powdered coal and the binder are mixed and stirred by the plurality of wire-mesh-like stirring blades provided in the pipe. Therefore, the pulverized coal can be moved differently from existing equipment, and pulverized coal with a wide range of particle sizes can be effectively granulated.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本考案の一実施例の一部切欠正面図、
第2図は第1図のA−A矢視拡大図、第3図は他
の実施例の一部切欠正面図、第4図はその底面
図、第5図は撹拌翼の他の実施例を示す図であ
る。 1,11……管、2,13……軸体、3,12
……撹拌翼。
FIG. 1 is a partially cutaway front view of an embodiment of the present invention.
Fig. 2 is an enlarged view taken along arrow A-A in Fig. 1, Fig. 3 is a partially cutaway front view of another embodiment, Fig. 4 is a bottom view thereof, and Fig. 5 is another embodiment of the stirring blade. FIG. 1,11...Pipe, 2,13...Shaft body, 3,12
...Agitation blade.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 管路中に、該管路軸心に一致すると共に駆動装
置に接続されて回転可能な軸体を設け、該軸体の
複数箇所に金網状の撹拌翼を取り付け且つ該撹拌
翼外周端と前記管路内周面との間に隙間を有せし
めた事を特徴とする粉炭の造粒装置。
A rotatable shaft that coincides with the axis of the pipe and is connected to a drive device is provided in the pipe, and wire-mesh-like stirring blades are attached to multiple locations on the shaft, and the outer peripheral end of the stirring blade and the A pulverized coal granulation device characterized by having a gap between the inner peripheral surface of the pipe and the inner peripheral surface of the pipe.
JP5129880U 1980-03-28 1980-04-15 Expired JPS6244742Y2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP5129880U JPS6244742Y2 (en) 1980-04-15 1980-04-15
US06/247,188 US4401278A (en) 1980-03-28 1981-03-24 Apparatus for granulating coal
GB8109521A GB2073649B (en) 1980-03-28 1981-03-26 Granulating apparatus
DE3111854A DE3111854C2 (en) 1980-03-28 1981-03-26 Granulator
CA000374078A CA1162045A (en) 1980-03-28 1981-03-27 Method of agglomeration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5129880U JPS6244742Y2 (en) 1980-04-15 1980-04-15

Publications (2)

Publication Number Publication Date
JPS56151350U JPS56151350U (en) 1981-11-13
JPS6244742Y2 true JPS6244742Y2 (en) 1987-11-27

Family

ID=29646210

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5129880U Expired JPS6244742Y2 (en) 1980-03-28 1980-04-15

Country Status (1)

Country Link
JP (1) JPS6244742Y2 (en)

Also Published As

Publication number Publication date
JPS56151350U (en) 1981-11-13

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